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    IMPROVED PROCESS AND CATALYST STRUCTURE EMPLOYING INTEGRAL HEAT EXCHANGE WITH OPTIONAL DOWNSTREAM FLAMEHOLDER
    36.
    发明申请
    IMPROVED PROCESS AND CATALYST STRUCTURE EMPLOYING INTEGRAL HEAT EXCHANGE WITH OPTIONAL DOWNSTREAM FLAMEHOLDER 审中-公开
    改进的工艺和催化剂结构采用整体热交换器与可选下游火焰探测器

    公开(公告)号：WO1995023915A1

    公开(公告)日：1995-09-08

    申请号：PCT/US1995001989

    申请日：1995-02-28

    Applicant: CATALYTICA, INC. ,  TANAKA KIKINZOKU KOGYO K.K.

    Inventor： CATALYTICA, INC. ,  TANAKA KIKINZOKU KOGYO K.K. ,  DALLA BETTA, Ralph, A. ,  SHOJI, Toru ,  YEE, David, K. ,  MAGNO, Scott, A.

    IPC: F01N03/10

    CPC classification number: F23C13/00 ,  F01N3/28 ,  F01N3/281 ,  F01N3/2814 ,  F01N3/2821 ,  F01N3/2882 ,  F01N2240/02 ,  F01N2330/321 ,  F01N2330/323 ,  F01N2330/42 ,  F23C6/045 ,  F23C9/006 ,  F23C2900/13002

    Abstract: The invention is an improved catalyst structure and its use in highly exothermic processes like catalyst combustion. This improved catalyst structure employed integral heat exchange in an array of longitudinally disposed, adjacent reaction passage-ways or channels, which are either catalyst-coated (14) or catalyst-free (16), wherein the configuration of the catalyst-coated channels (14) differ from the non-catalyst channels (16) such that, when applied in exothermic reaction processes, such as catalyst combustion, the desired reaction is promoted in the catalytic channels (14) and substantially limited in the non-catalytic channels (16). The invention further comprises an improved reaction system and process for combustion of a fuel wherein catalytic combustion using a catalyst structure employing integral heat exchange, preferably the improved structures of the invention, affords a partially-combusted, gaseous product which is passed to a homogeneous combustion zone where complete combustion is promoted by means of a flameholder.

    Abstract translation: 本发明是改进的催化剂结构及其在高度放热过程如催化剂燃烧中的应用。 这种改进的催化剂结构在纵向设置的相邻反应通道或通道的阵列中采用整体热交换，其是催化剂涂覆的（14）或无催化剂（16），其中催化剂涂覆的通道（ 14）与非催化剂通道（16）不同，使得当用于放热反应过程如催化剂燃烧时，在催化通道（14）中促进所需的反应，并且在非催化通道（16）中基本受限 ）。 本发明还包括改进的燃料燃烧反应系统和方法，其中使用采用整体热交换的催化剂结构的催化燃烧，优选本发明的改进结构，提供部分燃烧的气态产物，其被传递到均匀燃烧 通过火焰稳定器促进完全燃烧的区域。

    IMPROVED LEWIS ACID PROMOTED TRANSITION ALUMINA CATALYSTS AND ISOPARAFFIN ALKYLATION PROCESSES USING THOSE CATALYSTS
    38.
    发明申请
    IMPROVED LEWIS ACID PROMOTED TRANSITION ALUMINA CATALYSTS AND ISOPARAFFIN ALKYLATION PROCESSES USING THOSE CATALYSTS 审中-公开
    改进的LEWIS酸促进过渡氧化铝催化剂和使用这些催化剂的异噻唑烷基化方法

    公开(公告)号：WO1994002243A1

    公开(公告)日：1994-02-03

    申请号：PCT/US1993006712

    申请日：1993-07-16

    Applicant: CATALYTICA, INC.

    Inventor： CATALYTICA, INC. ,  COOPER, Michael, D. ,  KING, David, L. ,  SANDERSON, William, A.

    IPC: B01J21/02

    CPC classification number: B01J27/12 ,  B01J27/125 ,  C07C2/60 ,  C07C2521/04 ,  C07C2527/1213

    Abstract: This invention is directed to a catalyst system for use in the alkylation of isoparaffin with olefins. More specifically, this invention is directed to an improved catalyst system containing specified amounts of water and a component of that system comprising certain transition aluminas promoted with a Lewis acid (preferably BF3). In addition, this invention is a catalytic process for the alkylation of isoparaffin with olefins. The catalyst component is produced by contacting the transition alumina with the Lewis acid at relatively low temperatures. The catalyst system comprises that component and an additional amount of free Lewis acid. The process entails isoparaffin alkylation with olefins using the catalyst component and its allied catalyst system.

    Abstract translation: 本发明涉及一种用于烯烃与异链烷烃烷基化反应的催化剂体系。 更具体地，本发明涉及一种改进的催化剂体系，其包含特定量的水和该系统的组分，其包含用路易斯酸（优选BF 3）促进的某些过渡氧化铝。 此外，本发明是用烯烃烷基化异链烷烃的催化方法。 催化剂组分通过在较低温度下使过渡氧化铝与路易斯酸接触来制备。 催化剂体系包含该组分和另外量的游离路易斯酸。 该方法需要使用催化剂组分及其联合催化剂体系使烯烃进行异链烷烃化。

    DESULFURIZATION PROCESS USING BROMINE
    39.
    发明申请
    DESULFURIZATION PROCESS USING BROMINE 审中-公开
    使用溴的脱硫工艺

    公开(公告)号：WO1993020008A1

    公开(公告)日：1993-10-14

    申请号：PCT/US1993003143

    申请日：1993-04-02

    Applicant: CATALYTICA, INC.

    Inventor： CATALYTICA, INC. ,  SCHUBERT, Paul, F. ,  SCHUBERT, David, W. ,  MAHAJAN, Suresh ,  ROSTRUP-NIELSEN, Thomas

    IPC: C01B17/20

    CPC classification number: B01D53/507 ,  B01D53/73 ,  C01B17/74

    Abstract: This invention is a combination process for removal of sulfur oxides (SOx) from gases containing both the SOx and oxygen (106). The fluid used to remove the SOx contains sulfuric acid and bromine. The SOx is converted to sulfuric acid and the bromine is thereafter converted to hydrobromic acid. The hydrobromic acid is concentrated and catalytically converted to bromine for ultimate recycling to the SOx removal step (132). The SOx is finally recovered as a strong sulfuric acid (104).

    Abstract translation: 本发明是从含有SO x和氧（106）的气体中除去硫氧化物（SOx）的组合方法。 用于除去SOx的流体含有硫酸和溴。 将SO x转化为硫酸，然后将溴转化为氢溴酸。 将氢溴酸浓缩并催化转化成溴，以最终循环至SO x去除步骤（132）。 SO x最终作为强硫酸回收（104）。

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